Mass transport modeling of Cs(I) through hollow fiber supported liquid membrane containing calix-[4]-bis(2,3-naptho)-crown-6 as the mobile carrier

2011 ◽  
Vol 174 (1) ◽  
pp. 110-116 ◽  
Author(s):  
P. Kandwal ◽  
S. Dixit ◽  
S. Mukhopadhyay ◽  
P.K. Mohapatra
Keyword(s):  
Mass Transport ◽  
Hollow Fiber ◽  
Liquid Membrane ◽  
Transport Modeling ◽  
Supported Liquid Membrane ◽  
Mobile Carrier ◽  
Mass Transport Modeling

Separation and mass transport of Nd(III) from mixed rare earths via hollow fiber supported liquid membrane: Experiment and modeling

2014 ◽  
Vol 248 ◽  
pp. 158-167 ◽  
Author(s):  
Thanaporn Wannachod ◽  
Natchanun Leepipatpiboon ◽  
Ura Pancharoen ◽  
Kasidit Nootong
Keyword(s):  
Mass Transport ◽  
Rare Earths ◽  
Hollow Fiber ◽  
Liquid Membrane ◽  
Supported Liquid Membrane

Three-dimensional mass transport modeling of pharmaceuticals adsorption inside ZnAl/biochar composite

2021 ◽  
Vol 614 ◽  
pp. 126170
Author(s):  
Jaime Moreno-Pérez ◽  
Paola S. Pauletto ◽  
Anaelise M. Cunha ◽  
Ádrian Bonilla-Petriciolet ◽  
Nina P.G. Salau ◽  
...  
Keyword(s):  
Mass Transport ◽  
Three Dimensional ◽  
Transport Modeling ◽  
Mass Transport Modeling

Mass Transport Modeling in a Gas Antisolvent Process

2004 ◽  
Vol 43 (16) ◽  
pp. 4935-4943 ◽  
Author(s):  
Nicola Elvassore ◽  
Federico Cozzi ◽  
Alberto Bertucco
Keyword(s):  
Mass Transport ◽  
Transport Modeling ◽  
Mass Transport Modeling ◽  
Gas Antisolvent

scholarly journals Copper recovery in a bench-scale carrier facilitated tubular supported liquid membrane system

2010 ◽  
Vol 46 (1) ◽  
pp. 67-73 ◽  
Author(s):  
S. Makaka ◽  
M. Aziz ◽  
A. Nesbitt
Keyword(s):  
Sherwood Number ◽  
Liquid Membrane ◽  
Copper Ions ◽  
Membrane System ◽  
Copper Recovery ◽  
Supported Liquid Membrane ◽  
Shell Side ◽  
Copper Solution ◽  
Mobile Carrier ◽  
Double Pipe

The extraction of copper ions in a tubular supported liquid membrane using LIX 984NC as a mobile carrier was studied, evaluating the effect of the feed characteristics (flowrate, density, viscosity) on the feedside laminar layer of the membrane. A vertical countercurrent, double pipe perspex benchscale reactor consisting of a single hydrophobic PVDF tubular membrane mounted inside was used in all test work. The membrane was impregnated with LIX 984NC and became the support for this organic transport medium. Dilute Copper solution passed through the centre pipe and sulphuric acid as strippant passed through the shell side. Copper was successfully transported from the feedside to the stripside and from the data obtained, a relationship between Schmidt, Reynolds and Sherwood number was achieved of.

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